JPH0732379A - Manufacture of biodegradable resin foam - Google Patents
Manufacture of biodegradable resin foamInfo
- Publication number
- JPH0732379A JPH0732379A JP5201094A JP20109493A JPH0732379A JP H0732379 A JPH0732379 A JP H0732379A JP 5201094 A JP5201094 A JP 5201094A JP 20109493 A JP20109493 A JP 20109493A JP H0732379 A JPH0732379 A JP H0732379A
- Authority
- JP
- Japan
- Prior art keywords
- biodegradable resin
- resin
- foam
- mold
- biodegradable
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 229920006167 biodegradable resin Polymers 0.000 title claims abstract description 59
- 239000006260 foam Substances 0.000 title claims abstract description 24
- 238000004519 manufacturing process Methods 0.000 title claims description 10
- 238000000465 moulding Methods 0.000 claims abstract description 27
- 239000002245 particle Substances 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 27
- 239000000463 material Substances 0.000 claims description 16
- 229920005989 resin Polymers 0.000 abstract description 13
- 239000011347 resin Substances 0.000 abstract description 13
- 238000000034 method Methods 0.000 abstract description 8
- 230000008018 melting Effects 0.000 abstract description 5
- 238000002844 melting Methods 0.000 abstract description 5
- 239000012530 fluid Substances 0.000 description 12
- 238000005187 foaming Methods 0.000 description 12
- 230000006837 decompression Effects 0.000 description 9
- 239000011148 porous material Substances 0.000 description 8
- 229920003002 synthetic resin Polymers 0.000 description 8
- 239000000057 synthetic resin Substances 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 6
- 238000002347 injection Methods 0.000 description 6
- 239000007924 injection Substances 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 210000000497 foam cell Anatomy 0.000 description 5
- 238000001746 injection moulding Methods 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 4
- 239000010419 fine particle Substances 0.000 description 4
- 239000008187 granular material Substances 0.000 description 4
- 230000007246 mechanism Effects 0.000 description 4
- 244000005700 microbiome Species 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 229920002472 Starch Polymers 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 239000008107 starch Substances 0.000 description 3
- 235000019698 starch Nutrition 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000009423 ventilation Methods 0.000 description 3
- 208000031481 Pathologic Constriction Diseases 0.000 description 2
- 239000004372 Polyvinyl alcohol Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000011324 bead Substances 0.000 description 2
- 238000006065 biodegradation reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 239000011810 insulating material Substances 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- 229920002451 polyvinyl alcohol Polymers 0.000 description 2
- 238000004080 punching Methods 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 230000036262 stenosis Effects 0.000 description 2
- 208000037804 stenosis Diseases 0.000 description 2
- 239000000454 talc Substances 0.000 description 2
- 229910052623 talc Inorganic materials 0.000 description 2
- 239000004382 Amylase Substances 0.000 description 1
- 102000013142 Amylases Human genes 0.000 description 1
- 108010065511 Amylases Proteins 0.000 description 1
- 229920000856 Amylose Polymers 0.000 description 1
- 108010059892 Cellulase Proteins 0.000 description 1
- 229920001661 Chitosan Polymers 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 239000004367 Lipase Substances 0.000 description 1
- 102000004882 Lipase Human genes 0.000 description 1
- 108090001060 Lipase Proteins 0.000 description 1
- 239000004687 Nylon copolymer Substances 0.000 description 1
- 108091005804 Peptidases Proteins 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- 239000004365 Protease Substances 0.000 description 1
- 239000004373 Pullulan Substances 0.000 description 1
- 229920001218 Pullulan Polymers 0.000 description 1
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229920003232 aliphatic polyester Polymers 0.000 description 1
- 235000019418 amylase Nutrition 0.000 description 1
- 229920002988 biodegradable polymer Polymers 0.000 description 1
- 239000004621 biodegradable polymer Substances 0.000 description 1
- 230000031018 biological processes and functions Effects 0.000 description 1
- 229940106157 cellulase Drugs 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 229940088598 enzyme Drugs 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 239000004088 foaming agent Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 235000019421 lipase Nutrition 0.000 description 1
- 239000012778 molding material Substances 0.000 description 1
- 229920005615 natural polymer Polymers 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000006303 photolysis reaction Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920000570 polyether Polymers 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 235000019423 pullulan Nutrition 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 229920003179 starch-based polymer Polymers 0.000 description 1
- 239000004628 starch-based polymer Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Landscapes
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
- Biological Depolymerization Polymers (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、合成樹脂に代って脚光
を浴びてきた生分解性樹脂についての発泡体を製造する
方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a foam of a biodegradable resin which has been spotlighted in place of synthetic resin.
【0002】[0002]
【従来の技術】一般に普通の合成樹脂は、量産性、成形
性及び耐久性に優れているため多岐の分野に亘って使用
されており、なかでも合成樹脂の発泡体は、軽量で緩衝
性が高いことからガラス製品などの壊れ易い物の保護ケ
ース、運搬物の梱包用緩衝材、飲食用容器更には断熱材
や防音材などに用いられている。ところが合成樹脂品の
廃棄量が莫大になってきたため、種々の問題が提起され
ている。2. Description of the Related Art Generally, ordinary synthetic resins are used in a wide variety of fields because they are excellent in mass productivity, moldability, and durability. Among them, synthetic resin foams are lightweight and have a buffer property. Due to its high price, it is used as a protective case for fragile objects such as glassware, as a cushioning material for packing transported goods, as a food and drink container, as well as as a heat insulating material and soundproofing material. However, since the amount of synthetic resin products to be discarded has become huge, various problems have been raised.
【0003】即ち合成樹脂は焼却されると大量の有害ガ
スを発生して大気を汚染するし、またそのまま廃棄され
た場合には酸化や光分解が起こらないため長年その形状
を維持し、環境を汚染する。更に合成樹脂は分子間結合
力が非常に強いため、焼却した場合には高熱を発して炉
壁の使用寿命を短かくしてしまう。That is, when a synthetic resin is incinerated, a large amount of harmful gas is generated to pollute the atmosphere, and when it is discarded as it is, oxidation and photodecomposition do not occur, so that its shape is maintained for many years, and the environment is maintained. To contaminate. Further, since the synthetic resin has a very strong intermolecular bonding force, when it is incinerated, it generates high heat and shortens the service life of the furnace wall.
【0004】このようなことから最近において生分解性
樹脂が注目されてきており、その開発が盛んに行われて
いる。この生分解性樹脂は、例えばデンプン系高分子を
配合してなるものであって、土中や水中の微生物により
分解されるため、廃棄物対策として非常に有効なもので
ある。For these reasons, biodegradable resins have recently attracted attention and have been actively developed. This biodegradable resin is, for example, one containing a starch-based polymer and is decomposed by microorganisms in the soil or water, and therefore is very effective as a waste countermeasure.
【0005】そして生分解性樹脂の加工技術に関して
は、現在フィルム材の加工技術が実用化されつつある
が、発泡化についても実現できればその用途が非常に広
がり、生分解性樹脂の有利点をより活用することができ
る。ここに樹脂を発泡する技術としては、例えばスチレ
ンビーズを成形型の中に投入し、水蒸気を加えた後減圧
して発泡ビーズ群を得る方法や、押出機の中に例えばス
チレン樹脂を有機溶剤などの発泡剤と共に投入し、樹脂
が押し出されたときの減圧作用により発泡させる方法な
どが知られている。Regarding the processing technology of the biodegradable resin, the processing technology of the film material is currently being put to practical use, but if foaming can also be realized, its application will be greatly expanded, and the advantages of the biodegradable resin will be further enhanced. Can be utilized. Examples of the technique for foaming the resin include a method of charging styrene beads into a molding die, adding steam and then depressurizing to obtain a group of expanded beads, and an extruder such as an organic solvent of styrene resin. There is known a method in which the resin is added together with the foaming agent, and the resin is foamed by a depressurizing action when the resin is extruded.
【0006】[0006]
【発明が解決しようとする課題】しかしながら生分解性
樹脂は通常の合成樹脂と性状が異なるため種々の問題点
がある。その一つの問題点を述べると、生分解性樹脂は
加圧状態から解放されるや否や発泡を開始してしまう
が、生分解性樹脂が加熱されて流動状となっているとき
の粘度が大きいため、生分解性樹脂が成形型の奥まで入
り込みにくく、このため生分解性樹脂の一部はシリンダ
から押出されて金型の内面に到達する前に発泡してしま
い、この結果金型の隅部や入り組んだ個所においては本
来奥に達して発泡すべき部分が途中で発泡してその手前
に溜まりこれにより奥部に空隙が形成され、この状態で
続いて押し出された生分解性樹脂が前方の発泡部分を背
面から押圧し、これにより当該部分が押し潰されてしま
う。このように一旦発泡してもその部分が後方より押し
潰されてしまうと、所望の形状の発泡体が得られない
し、また十分な緩衝性能を有するものが得られない。However, since the biodegradable resin has different properties from ordinary synthetic resins, there are various problems. One of the problems is that the biodegradable resin starts foaming as soon as it is released from the pressurized state, but the viscosity is high when the biodegradable resin is heated and becomes fluid. Therefore, it is difficult for the biodegradable resin to enter the inside of the mold, and as a result, part of the biodegradable resin is extruded from the cylinder and foams before reaching the inner surface of the mold, resulting in a corner of the mold. In the parts and intricate parts, the part that should reach the inner part and should be foamed foams in the middle and collects in front of it, forming a void in the inner part, and in this state, the extruded biodegradable resin is forward. The foamed part of is pressed from the back side, and this part is crushed. Thus, if the portion is crushed from the rear side even if it is once foamed, a foam having a desired shape cannot be obtained, and a foam having sufficient cushioning performance cannot be obtained.
【0007】本発明は、このような事情のもとになされ
たものであり、その目的は、生分解性樹脂について発泡
セルの潰れを抑え、所望の形状で均質な発泡体を得るこ
とのできる生分解性樹脂発泡体の製造方法を提供するこ
とにある。The present invention has been made under such circumstances, and an object thereof is to suppress collapse of foam cells of a biodegradable resin and to obtain a uniform foam having a desired shape. It is to provide a method for producing a biodegradable resin foam.
【0008】[0008]
【課題を解決するための手段】本発明は、前方に狭窄開
口を有する筒状容器内に実質的に水分と生分解性樹脂と
を投入し、生分解性樹脂を前記狭窄開口に押送する間に
昇温せしめて加熱加圧状態の流動状物とし、この加熱加
圧状態の流動状物を前記狭窄開口から通気性の成形型内
に霧化状態で射出して霧化状態の生分解性樹脂粒子を発
泡させ、成形型に応じた形状に成形することを特徴とす
る。According to the present invention, while substantially inserting water and a biodegradable resin into a cylindrical container having a stenosis opening at the front, and pushing the biodegradable resin to the stenosis opening. The fluid is heated and pressurized to form a fluid under heating and pressurization, and the fluid under heating and pressurization is injected from the constriction opening into the air-permeable mold in an atomized state and biodegradable in the atomized state. It is characterized in that resin particles are foamed and molded into a shape corresponding to a molding die.
【0009】[0009]
【作用】生分解性樹脂は狭窄開口に押送する間に例えば
軟化点ないし融点程度に昇温せしめられて加熱加圧状態
の流動状物となり、同時に存在する水分は加圧状態下で
あって沸点が上昇するため流動状の生分解性樹脂から蒸
発することなくその中に閉じ込められた状態となってい
る。この加熱加圧状態の流動状物を狭窄開口から通気性
の成形型内に霧化状態で射出すると、霧化状態の生分解
性樹脂粒子が成形型内の隅々まで行き渡ると共に加熱加
圧状態から急激に解放されて今まで内部に閉じ込められ
ていた水分が一気に蒸発しようとして膨張拡大し、蒸発
した水分は通気性の成形型外に放散される一方、霧化状
態の生分解性樹脂が各々発泡して集合し、発泡セルが押
し潰されることなく所望の形状で均質な発泡体が得られ
る。The biodegradable resin is heated to, for example, the softening point or the melting point while being pushed into the constriction opening to become a fluid under heating and pressurization, and the water present at the same time has a boiling point under pressurization. As a result, the fluidized biodegradable resin is trapped inside the biodegradable resin without evaporating. When this fluidized material in the heated and pressurized state is injected from the narrowed opening into the air-permeable molding die in an atomized state, the biodegradable resin particles in the atomized state spread to every corner of the molding die and are heated and pressurized. The water that was suddenly released from the mold was expanded and expanded in an attempt to evaporate at once, and the evaporated water was dissipated outside the breathable mold, while the atomized biodegradable resin It foams and collects, and a foam having a desired shape and homogeneous can be obtained without crushing the foam cells.
【0010】[0010]
【実施例】以下に本発明の実施例について説明するが、
具体的な製法について述べる前に先ず生分解性樹脂につ
いて説明する。生分解性樹脂とは生物学的作用に基づき
物性を低下する樹脂材料を意味し、これには樹脂自体が
完全に分解するタイプと、分解し難い樹脂とブレンドし
崩壊性を付与したタイプとがある。そして、前者のタイ
プには微生物による生産物、天然高分子の利用品、石油
系原料からの生成品等があり、また、後者のタイプには
デンプンとのブレンド体、脂肪族ポリエステルとのブレ
ンド体等がある。これらの生分解機構としては、リパー
ゼ、アミラーゼ、セルラーゼ、プロテアーゼ等の酵素に
よる分解、活性汚泥中等の微生物による分解、森林や耕
作地等の自然環境における土壌による分解等、種々の態
様がある。EXAMPLES Examples of the present invention will be described below.
Before describing a specific manufacturing method, the biodegradable resin will be described first. A biodegradable resin means a resin material whose physical properties are deteriorated based on a biological action.There are two types: a type in which the resin itself is completely decomposed and a type in which a resin that is difficult to decompose is blended to provide disintegration. is there. The former type includes products produced by microorganisms, products using natural polymers, products produced from petroleum-based raw materials, and the latter type includes blends with starch and blends with aliphatic polyesters. Etc. These biodegradation mechanisms include various modes such as decomposition by enzymes such as lipase, amylase, cellulase, and protease, decomposition by microorganisms such as activated sludge, and decomposition by soil in natural environments such as forests and cultivated lands.
【0011】更に具体的には、ポリヒドロキシ酪酸及び
その誘導体、プルラン、セルロース−キトサン混合体、
セルロースやアミロースや木粉のエステル化物、ポリエ
ステル−ナイロン共重合体、ポリエステル共重合体、デ
ンプンとポリエチレンとのブレンド体をはじめ、ポリビ
ニルアルコール、ポリエーテル、ポリウレタン、ポリア
ミド等が挙げられる。これらはおしなべて低融点を有
し、水の存在下に分解促進されるものである。More specifically, polyhydroxybutyric acid and its derivatives, pullulan, cellulose-chitosan mixture,
Examples thereof include esterified products of cellulose, amylose and wood flour, polyester-nylon copolymers, polyester copolymers, blends of starch and polyethylene, polyvinyl alcohol, polyether, polyurethane and polyamide. These generally have low melting points and are accelerated in the presence of water.
【0012】そして、本実施例では、生分解性樹脂に日
本合成化学工業株式会社販売のMater−Bi「マタ
ービー」(登録商標)のペレット状のものを用いたが、
これは、イタリアのモンテジソングループに属するNO
VAMONT社の開発に係り、デンプンなどの複数農産
物からの誘導品と変性ポリビニルアルコールとが分子レ
ベルで相互に相手分子中に潜り込み、水素結合により結
ばれてなる、熱可塑性の生分解性ポリマーとされている
ものである。また、水を吸収して膨潤することにより生
分解促進され、微生物生存の環境下で紙と同等の生分解
性を示すとされている。In this embodiment, the biodegradable resin used was Mater-Bi "Matterby" (registered trademark) pellets sold by Nippon Synthetic Chemical Industry Co., Ltd.
This is a NO belonging to the Montedison Group in Italy
In connection with the development of VAMONT, it is considered to be a thermoplastic biodegradable polymer in which derivative products from multiple agricultural products such as starch and denatured polyvinyl alcohol infiltrate into each other at the molecular level and are bonded by hydrogen bonds. It is what Further, it is said that biodegradation is promoted by absorbing water and swelling, and exhibits biodegradability equivalent to that of paper in an environment in which microorganisms survive.
【0013】また、生分解性樹脂と水分とを後述の筒状
容器内に投入するためには、発泡用の生分解性樹脂ペレ
ットを成形するときに予め適度の水分を含有させるよう
にしてもよいし、あるいは例えば生分解性樹脂の粒体に
水を積極的に含水させる前処理工程を設けてもよい。ま
た生分解性樹脂とともに水そのものをホッパ内に直接添
加してもよいし、ニーダを介してシリンダ内に供給して
もよく、実質的に生分解性樹脂と水分とが供給されさえ
すればよい。Further, in order to put the biodegradable resin and the water into a cylindrical container described later, an appropriate amount of water may be contained in advance when molding the biodegradable resin pellet for foaming. Alternatively, for example, a pretreatment step of positively containing water in the biodegradable resin granules may be provided. Further, water itself may be added directly into the hopper together with the biodegradable resin, or may be supplied into the cylinder through a kneader, as long as the biodegradable resin and water are substantially supplied. .
【0014】また予め水分を吸湿させた吸湿性の微粒子
状物質例えばタルク(滑石)やシリカを生分解性樹脂に
添加しておけば、これら微粒子状物質は樹脂との相溶
性、分散性が水の直接添加よりは高いため、また、発泡
時には微粒子中の水分がその微粒子を起点として発泡し
得るので、結果として微細かつ均一に発泡した発泡体が
得られる。Further, if a hygroscopic fine particle substance which has absorbed moisture in advance, such as talc (talc) or silica, is added to the biodegradable resin, the fine particle substance has water compatibility and dispersibility with the resin. Since it is higher than that of direct addition, and the water content in the fine particles can be foamed starting from the fine particles at the time of foaming, as a result, a finely and uniformly foamed product can be obtained.
【0015】次に本発明の実施例で用いる製造装置につ
いて図1を参照しながら述べると、1は筒状容器に相当
するシリンダであり、後端部上方には成形材料投入用の
ホッパ11が設けられている。このシリンダ1の先端部
には、先端が狭窄開口をなすノズル12が形成されると
共に、シリンダ1の周囲には加熱用のヒータ13が配置
されている。Next, a manufacturing apparatus used in the embodiment of the present invention will be described with reference to FIG. 1. Reference numeral 1 is a cylinder corresponding to a cylindrical container, and a hopper 11 for charging a molding material is provided above a rear end portion thereof. It is provided. A nozzle 12 having a narrowed opening at the tip is formed at the tip of the cylinder 1, and a heater 13 for heating is arranged around the cylinder 1.
【0016】前記シリンダ1内には、前後方向に伸びる
スクリュー2がその内壁に近接して配設されており、こ
のスクリュー2の後端はシリンダ1の後端開口部より後
方側に延び出して、スクリュー2を回転させるための油
圧モータ21に接続されている。更に油圧モータ21の
後部には、射出シリンダ22内に摺動自在に配置された
ピストン23が取り付けられており、従って油圧により
ピストン23、油圧モータ21及びスクリュー2が一体
となって前後方向に移動すると共に、スクリュー2は油
圧モータ21により回転する。Inside the cylinder 1, a screw 2 extending in the front-rear direction is arranged close to the inner wall thereof, and the rear end of the screw 2 extends rearward from the rear end opening of the cylinder 1. , Is connected to a hydraulic motor 21 for rotating the screw 2. Further, a piston 23 slidably arranged in the injection cylinder 22 is attached to the rear part of the hydraulic motor 21, and therefore the piston 23, the hydraulic motor 21 and the screw 2 are integrally moved by the hydraulic pressure in the front-rear direction. At the same time, the screw 2 is rotated by the hydraulic motor 21.
【0017】こうしていわゆるインラインスクリュー式
射出成形機が構成され、この成形機の先端には通気性の
成形型Aが配置されており、この成形型Aは、固定側ダ
イセット7を介してノズル12の開口(狭窄開口)に連
通するキャビティ31が形成された固定側金型3と、コ
ア41が形成された可動側金型4とから構成されてい
る。この実施例ではキャビティ31は例えば方形状をな
し、またコア41は例えば方形状の一面に小さな方形状
の凸部を有する形状をなしており、両金型3、4を型締
めしたと成形型Aに対応する形状の発泡品が得られるよ
うになっている。A so-called in-line screw type injection molding machine is constructed in this way, and a breathable molding die A is arranged at the tip of this molding machine. This molding die A is provided with a nozzle 12 via a stationary die set 7. Of the fixed side mold 3 in which the cavity 31 communicating with the opening (narrowing opening) is formed, and the movable side mold 4 in which the core 41 is formed. In this embodiment, the cavity 31 has, for example, a square shape, and the core 41 has, for example, a shape having a small square convex portion on one surface of the square shape. A foamed product having a shape corresponding to A can be obtained.
【0018】そして前記成形型Aには型締め機構が組み
合わせて設けられ、この型締め機構は、例えば可動側金
型4を固定側金型3と対向しつつ接離するようにガイド
するタイバー42、43や可動側金型4を接離動作させ
るための作動機構44などから構成されている。The mold A is provided with a mold clamping mechanism in combination, and the mold clamping mechanism guides the movable side mold 4 so as to contact and separate the movable side mold 4 while facing the fixed side mold 3, for example. , 43 and an operating mechanism 44 for moving the movable side mold 4 into and out of contact with each other.
【0019】ここでノズル12の口径は、加熱加圧状態
の流動状物をノズル12から霧化状態でキャビティ31
とコア41とにより形成される成形空間に射出するため
に従来の一般の射出成形機のノズルよりも小径とするこ
とが必要である。即ち従来の一般の射出成形機のノズル
の口径は例えば2〜5mmとされているが、この実施例
では例えばノズル12の口径を1mm程度の小径なもの
としている。Here, the diameter of the nozzle 12 is such that the fluid material in the heated and pressurized state is atomized from the nozzle 12 into the cavity 31.
In order to inject into the molding space formed by the core 41 and the core 41, it is necessary to make the diameter smaller than that of the nozzle of the conventional general injection molding machine. That is, the diameter of the nozzle of the conventional general injection molding machine is set to, for example, 2 to 5 mm, but in this embodiment, for example, the diameter of the nozzle 12 is set to a small diameter of about 1 mm.
【0020】前記成形型Aは、ほぼ全体において内外を
連通する無数の網組織状の孔を有する多孔質材から成っ
ている。この多孔質材としては、発泡金属がある他、空
隙を形成し得る充填材を添加して焼結成形した金属又は
セラミックス等の焼結物、更には金網、パンチングメタ
ル等をプレス賦形しそれらを積層してなるもの等を使用
することができ、簡易な構造としては、1枚板のパンチ
ングメタルを所定の形状に成形したものも使用できる。
ここで多孔質材の孔が大きいと、蒸気の排出効率及び通
風効率が良いが、あまり大きくすると発泡後の成形体の
表面に孔による凹凸が強く出て表面が荒れる。このため
多孔質材の孔の大きさは、成形体の用途に応じた表面の
平滑性が得られる範囲内であって、通気抵抗があまり大
きくならない範囲に設定され、好適なものとしては孔径
の設定が容易でかつ構造が簡易であることなどからパン
チングメタルを用いたものを挙げることができる。The molding die A is made of a porous material having an infinite number of network-like pores that communicate the inside and the outside almost all over. As the porous material, there are foamed metal, sintered materials such as metal or ceramics sintered by adding a filler capable of forming voids, metal wire, punching metal, etc. Can be used, and as a simple structure, a single punched metal formed into a predetermined shape can also be used.
Here, if the pores of the porous material are large, the steam discharge efficiency and the ventilation efficiency are good, but if they are too large, the surface of the molded body after foaming becomes strongly uneven due to the pores and the surface becomes rough. Therefore, the size of the pores of the porous material is set within a range in which the smoothness of the surface according to the use of the molded article is obtained, and the range in which the ventilation resistance does not become too large. One using punching metal can be mentioned because it is easy to set and has a simple structure.
【0021】以上のような構成の製造装置を用いて本発
明の製造方法を説明すると、先ず成形型Aを型締めして
おき、ホッパ11内に生分解性樹脂の粒体10を供給
し、図2(a)に示すように、スクリュー2によりシリ
ンダ1内を前方に押送せしめる。生分解性樹脂の粒体1
0は、押送される間に、スクリュー2の回転に伴う剪断
力及びヒータ13によるシリンダ1の内壁からの加熱に
より軟化点または融点程度の温度に昇温され、スクリュ
ー2の先端側におけるシリンダ1の内部空間に流動状物
になって溜まる。このとき当該内部空間は加熱加圧状態
となって、生分解性樹脂の粒体10に含まれていた水分
はその流動状物から蒸発することなくその中に閉じ込め
られた状態となっている。The manufacturing method of the present invention will be described using the manufacturing apparatus configured as described above. First, the mold A is clamped, and the biodegradable resin granules 10 are fed into the hopper 11. As shown in FIG. 2A, the inside of the cylinder 1 is pushed forward by the screw 2. Granules of biodegradable resin 1
0 is heated to a temperature around the softening point or the melting point due to the shearing force accompanying the rotation of the screw 2 and the heating from the inner wall of the cylinder 1 by the heater 13 while being pushed, It collects as a fluid in the internal space. At this time, the internal space is heated and pressurized, and the water contained in the granules 10 of the biodegradable resin is trapped in the fluidized material without evaporating from the fluidized material.
【0022】続いて、図2(b)に示すように,スクリ
ュー2の回転を止め、射出シリンダ22内のピストン2
3を稼働してスクリュー2を前進させ、流動状物をノズ
ル12から成形型A内のキャビティ31とコア41とに
より形成される成形空間内に霧化状態で一気に噴射す
る。Then, as shown in FIG. 2B, the rotation of the screw 2 is stopped and the piston 2 in the injection cylinder 22 is stopped.
3 is operated to move the screw 2 forward, and the fluid material is injected from the nozzle 12 into the molding space formed by the cavity 31 and the core 41 in the molding die A in an atomized state.
【0023】ここで霧化状態で噴射するためには、上述
のようにノズル12の口径を従来一般のものよりも小径
としたうえ、スクリュー2による流動状物の射出速度
と、当該流動状物の押し出し前後の圧力差を適宜調整す
ればよい。なお霧化状態とするために必要なノズル12
の口径は流動状物の押し出し速度によっても変動するの
で、上述のように1mm程度に限定されるものではな
い。In order to inject in the atomized state, the nozzle 12 has a smaller diameter than the conventional one as described above, and the injection speed of the fluid material by the screw 2 and the fluid material The pressure difference before and after the extrusion may be adjusted appropriately. It should be noted that the nozzle 12 required to make the atomized state
Since the diameter of the above varies depending on the extrusion speed of the fluid material, it is not limited to about 1 mm as described above.
【0024】一方、成形型Aの外部は大気に開放されて
いるので、通気性の成形型Aの多孔質部分を介してその
キャビティ31も大気圧となっている。従って霧化状態
でキャビティ31内に一気に射出された生分解性樹脂は
加熱加圧状態から急激に大気圧下に晒されることとなる
ので、これに閉じ込められていた水分が瞬間的に蒸発し
て発泡する。生分解性樹脂内にはこの水蒸気の膨張する
力が働くが、その最外郭は成形型Aに接しているためキ
ャビティ31とコア41の形状に規制される。そして水
蒸気は成形型Aの多孔質部分を通って外部に放散される
一方、生分解性樹脂内部の各粒子毎に発泡が行われて気
泡100(発泡セル)が形成され、これら粒子が絡み合
い、融着し合って全体が一つに賦形された生分解性樹脂
の発泡体Bが得られる。On the other hand, since the outside of the mold A is open to the atmosphere, the cavity 31 of the mold A is also at atmospheric pressure through the porous portion of the mold A. Therefore, the biodegradable resin that has been rapidly injected into the cavity 31 in the atomized state is rapidly exposed to the atmospheric pressure from the heating and pressurizing state, and the water trapped in this is instantaneously evaporated. Foam. The force of expansion of the water vapor works in the biodegradable resin, but the outermost portion of the biodegradable resin is in contact with the molding die A, so that the shapes of the cavity 31 and the core 41 are restricted. Then, the water vapor is diffused to the outside through the porous portion of the mold A, while foaming is performed for each particle inside the biodegradable resin to form a bubble 100 (foam cell), and these particles are entangled with each other. A foamed body B of biodegradable resin in which the whole is shaped into one by fusion bonding is obtained.
【0025】次いで図2(c)に示すようにスクリュー
2を回転させながら後退させるとその間に再度流動状と
なった生分解性樹脂がスクリュー2の先端側におけるシ
リンダ1の内部空間に溜まり始め、次の射出に備える。
この間に成形型A内のキャビティ31内では、成形後の
生分解性樹脂発泡体の冷却固化も完了するので成形型A
を型開きして発泡体Bを取り出し、再び型締めして次の
操作を行う。Next, as shown in FIG. 2 (c), when the screw 2 is rotated and retracted, the fluidized biodegradable resin begins to collect in the internal space of the cylinder 1 on the tip side of the screw 2 again. Prepare for the next shot.
During this time, in the cavity 31 in the molding die A, the cooling and solidification of the biodegradable resin foam after molding is completed, so the molding die A
The mold is opened, the foam B is taken out, the mold is clamped again, and the following operation is performed.
【0026】そして上述の方法では、流動状の生分解性
樹脂がノズル12から霧化状態で大気圧下のキャビティ
31内に射出されるので、霧化状態の生分解性樹脂粒子
がキャビティ31とコア41とにより形成される成形空
間内の隅々まで充填されると共に、各霧化状態の生分解
性樹脂粒子が各々発泡して集合する。このため生分解性
樹脂が成形型A内の隅々まで入り込んだ状態で発泡が完
了するので、成形型Aの形状が複雑であっても発泡セル
が型内面から浮いた位置に溜まって後方から生分解性樹
脂の押圧により無理に押し込まれて潰されるという不具
合を緩和あるいは回避することができ、従って一旦発泡
した発泡セルの押し潰しを抑えることができるので所望
の形状で均質な発泡体を得ることができ、この結果十分
な緩衝性能を得ることができる。In the above method, since the fluid biodegradable resin is ejected from the nozzle 12 into the cavity 31 under the atmospheric pressure in the atomized state, the atomized biodegradable resin particles form the cavity 31. While being filled up in every corner of the molding space formed by the core 41, the biodegradable resin particles in each atomized state foam and aggregate. Therefore, since the foaming is completed with the biodegradable resin entering every corner of the mold A, even if the mold A has a complicated shape, the foam cells are accumulated in the position floating from the inner surface of the mold and It is possible to mitigate or avoid the problem that the biodegradable resin is forced to be pressed and crushed, and therefore it is possible to suppress the crushing of the foam cells that have once foamed, so that a uniform foam with a desired shape can be obtained. As a result, sufficient cushioning performance can be obtained.
【0027】本発明においては、成形型Aの外部を通風
雰囲気としてもよく、この場合は水蒸気が成形型Aの外
に強制的に放出されるので、気化膨張して発泡に寄与し
た後の水分の再付着に起因する収縮を抑えられるという
利点がある。In the present invention, a ventilation atmosphere may be provided outside the molding die A. In this case, since water vapor is forcibly released to the outside of the molding die A, the water content after vaporizing and expanding and contributing to foaming is increased. There is an advantage that the contraction caused by the redeposition of the can be suppressed.
【0028】なお成形型Aを減圧チャンバーの内部に配
置して成形型Aの外部雰囲気を大気圧以下に減圧しても
よく、この場合は大きな圧力差が得られるので、より高
発泡化させることができると共に、水蒸気の強制放出作
用がより大きくなって成形型Aにおける結露が抑えられ
る。The molding die A may be placed inside the decompression chamber to reduce the pressure of the atmosphere outside the molding die A to atmospheric pressure or less. In this case, a large pressure difference can be obtained. At the same time, the action of forced release of water vapor is further increased, and dew condensation on the mold A is suppressed.
【0029】また本発明ではノズル12は1本に限定さ
れず、例えば図3に示すように複数のノズル12を設け
てもよいし、場合によっては図4に示すようにシリンダ
1の先端に多数の微細な噴射穴14を備えたシャワー部
15を設けてもよい。更に、図示しないが、ランナー、
ゲートを経由して成形型内に生分解性樹脂が導入される
場合には、ランナーやゲートの口径を小さくするなどし
て、生分解性樹脂が霧化状態で成形型内に導入されるよ
うにすればよい。In the present invention, the number of nozzles 12 is not limited to one, and a plurality of nozzles 12 may be provided, for example, as shown in FIG. 3. In some cases, a large number of nozzles 12 may be provided at the tip of the cylinder 1 as shown in FIG. You may provide the shower part 15 provided with the minute injection hole 14 of this. Furthermore, although not shown, a runner,
When biodegradable resin is introduced into the mold via the gate, reduce the diameter of the runner and gate so that the biodegradable resin is introduced into the mold in an atomized state. You can do this.
【0030】更に本発明では、図5に示すように互いに
気密な複数の減圧室51〜53に分割された減圧チャン
バー5を成形型Aを取り囲むように設けると共に、各室
に対応する減圧用配管61〜65を設け、各減圧用配管
による減圧の程度を変化させることにより、霧化状態の
生分解性樹脂粒子が成形空間の奥から効率良く順次に充
填されるように充填状態を調整するようにしてもよい。
この場合減圧チャンバー5は、例えば成形型Aと同時に
開閉できるように構成される。ここで、射出成形機のノ
ズルは開放されており、またシリンダの原料供給側のホ
ッパも開放されており、原料や溶融樹脂により有る程度
の密閉度が確保されるものの、シリンダ内の密閉性が低
いと加圧が不十分になり、生分解性樹脂の軟化点ないし
融点と加圧下の水の沸点との兼ね合いで射出前シリンダ
内にて一部の水分が気化し、発泡するおそれがあり、ま
たノズルから鼻垂れ状態で発泡することもある。そこで
本発明では、ノズルをバルブ付きのものにしたり、原料
供給部側のホッパを密閉したり、さらには原料供給口に
ロータリバルブを付設するなどして密閉性を高めること
が好ましい。また、例えばポリエチレングリコールなど
を溶質として水に溶かし、この水を添加するようにし
て、これにより水の沸点を上昇させ射出前シリンダ内発
泡を抑制するようにしてもよい。Further, in the present invention, as shown in FIG. 5, a decompression chamber 5 divided into a plurality of airtight decompression chambers 51 to 53 is provided so as to surround the molding die A, and decompression pipes corresponding to the respective chambers are provided. 61 to 65 are provided and the degree of decompression by each decompression pipe is changed so that the filling state is adjusted so that the biodegradable resin particles in the atomized state are efficiently and sequentially filled from the back of the molding space. You may
In this case, the decompression chamber 5 is configured so that it can be opened and closed at the same time as the molding die A, for example. Here, the nozzle of the injection molding machine is open, and the hopper on the raw material supply side of the cylinder is also open, and although a certain degree of tightness is secured by the raw material and the molten resin, the airtightness inside the cylinder is If the pressure is low, pressurization will be insufficient, and due to the balance between the softening point or melting point of the biodegradable resin and the boiling point of water under pressure, some water may vaporize in the cylinder before injection, causing foaming. In addition, foaming may occur from the nozzle in the dripping state. Therefore, in the present invention, it is preferable to improve the hermeticity by providing the nozzle with a valve, sealing the hopper on the side of the raw material supply section, and further attaching a rotary valve to the raw material supply port. Alternatively, for example, polyethylene glycol or the like may be dissolved in water as a solute, and this water may be added, whereby the boiling point of water may be raised and foaming in the cylinder before injection may be suppressed.
【0031】なお本発明により得られる生分解性樹脂発
泡体は、緩衝材としての用途に限定されるものではな
く、断熱材や防音材などに用いるものであってもよい。The biodegradable resin foam obtained by the present invention is not limited to the use as a cushioning material, but may be used as a heat insulating material, a soundproofing material or the like.
【0032】[0032]
【発明の効果】以上のように本発明によれば、生分解性
樹脂を均一に発泡させることができて適宜形状に成形す
ることができ、従来の合成樹脂の発泡体の代替品として
使用することによりゴミ公害などの環境汚染の軽減に寄
与することができる。As described above, according to the present invention, a biodegradable resin can be uniformly foamed and can be molded into an appropriate shape, and it can be used as a substitute for a conventional synthetic resin foam. This can contribute to the reduction of environmental pollution such as garbage pollution.
【図1】本発明方法の一実施例に用いられる製造装置の
一例を示す概略縦断面図である。FIG. 1 is a schematic vertical sectional view showing an example of a manufacturing apparatus used in an embodiment of the method of the present invention.
【図2】インラインスクリュー式射出成形機を用いて本
発明方法の一実施例を実施する様子を示す概略縦断面図
である。FIG. 2 is a schematic vertical cross-sectional view showing how an embodiment of the method of the present invention is carried out using an inline screw type injection molding machine.
【図3】複数のノズルを設けたシリンダ先端部の概略斜
視図である。FIG. 3 is a schematic perspective view of a cylinder tip portion provided with a plurality of nozzles.
【図4】シャワー部を設けたシリンダ先端部の概略斜視
図である。FIG. 4 is a schematic perspective view of a cylinder tip portion provided with a shower portion.
【図5】本発明方法を実施するための他の製造装置の要
部を示す概略縦断面図である。FIG. 5 is a schematic vertical sectional view showing a main part of another manufacturing apparatus for carrying out the method of the present invention.
A 成形型 B 発泡体 1 シリンダ 11 ホッパ 12 ノズル 2 スクリュー 23 ピストン 3 固定側金型 31 キャビティ 4 可動側金型 41 コア 5 減圧チャンバー 51、52、53 減圧室 A Mold B Foam 1 Cylinder 11 Hopper 12 Nozzle 2 Screw 23 Piston 3 Fixed Side Mold 31 Cavity 4 Movable Side Mold 41 Core 5 Decompression Chamber 51, 52, 53 Decompression Chamber
Claims (1)
質的に水分と生分解性樹脂とを投入し、生分解性樹脂を
前記狭窄開口に押送する間に昇温せしめて加熱加圧状態
の流動状物とし、この加熱加圧状態の流動状物を前記狭
窄開口から通気性の成形型内に霧化状態で射出して霧化
状態の生分解性樹脂粒子を発泡させ、成形型に応じた形
状に成形することを特徴とする生分解性樹脂発泡体の製
造方法。1. A water container and a biodegradable resin are substantially put into a cylindrical container having a constriction opening in the front, and the biodegradable resin is heated and pressurized while being pushed to the constriction opening. The fluidized material in the state of heat and pressure is injected from the constriction opening into the air-permeable molding die in the atomized state to foam the biodegradable resin particles in the atomized state, A method for producing a biodegradable resin foam, which comprises molding the biodegradable resin foam into a shape according to the above.
Priority Applications (10)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5201094A JPH0732379A (en) | 1993-07-20 | 1993-07-20 | Manufacture of biodegradable resin foam |
| US08/274,038 US5602188A (en) | 1993-07-13 | 1994-07-12 | Biodegradable resin foam and method and apparatus for producing same |
| DE69432606T DE69432606T2 (en) | 1993-07-13 | 1994-07-13 | Biodegradable foam |
| EP94305110A EP0634261B1 (en) | 1993-07-13 | 1994-07-13 | Method and apparatus for producing biodegradable resin foam |
| DE69406366T DE69406366T2 (en) | 1993-07-13 | 1994-07-13 | Method and device for producing a biodegradable foam |
| EP97200618A EP0785055B1 (en) | 1993-07-13 | 1994-07-13 | Biodegradable resin foam |
| SG1996008114A SG76470A1 (en) | 1993-07-13 | 1994-07-13 | Biodegradable resin foam and method and apparatus for producing same |
| US08/734,957 US5849339A (en) | 1993-07-13 | 1996-10-23 | Apparatus for producing biodegradable resin foam |
| US09/210,664 US6228898B1 (en) | 1993-07-13 | 1998-12-14 | Biodegradable resin foam and method and apparatus for producing same |
| US09/850,002 US6626654B1 (en) | 1993-07-13 | 2001-05-08 | Biodegradable resin foam and method and apparatus for producing same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5201094A JPH0732379A (en) | 1993-07-20 | 1993-07-20 | Manufacture of biodegradable resin foam |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0732379A true JPH0732379A (en) | 1995-02-03 |
Family
ID=16435302
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5201094A Pending JPH0732379A (en) | 1993-07-13 | 1993-07-20 | Manufacture of biodegradable resin foam |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0732379A (en) |
-
1993
- 1993-07-20 JP JP5201094A patent/JPH0732379A/en active Pending
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| Publication | Publication Date | Title |
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